Method for producing bodies of consolidated particulate material

ABSTRACT

Shaped bodies of particulate material produced by introducing an easily flowable slurry of water and particulate material into a mold with perforated walls and applying a sufficiently high pressure to the slurry in the mold so as to express a sufficient proportion of the liquid to allow physical contact and interengagement between the particles. The method may be carried out continuously in an extension process including: (A) introducing the slurry under high pressure, (B) conveying the slurry through a shaping section to (C) a draining and consolidation section with drain holds or slits ( 3 ), to leave the extruder through (E) an exit section in the form of a solid body ( 4 ).

CROSS REFERENCE TO RELATED APPLICATION

[0001] This application is a continuation of application Ser. No.08/765,905, filed Jan. 7, 1997, now U.S. Pat. No. 6,398,998; which is aUS national phase of PCT/DK95/00296 filed Jul. 5, 1995.

TECHNICAL FIELD

[0002] The present invention relates to a method for producing shapedbodies.

BACKGROUND ART

[0003] A method of this kind is disclosed in BE-A-653,349 andSE-B-304,711 (both based on FR priority application No. 955,561 of Nov.29, 1963). In this known method, an unhardened mixture comprisinghydraulic cement and aggregate material (sand and gravel) with surpluswater is compressed in an extruder of constant cross-sectional shape bymeans of a reciprocating piston, and in the terminal part of saidextruder, the walls of which are suitably perforated, part of the wateris removed by applying a vacuum to the outside of said walls, all thistaking place while the material is moving slowly through the extruder.

[0004] Obviously, the pressure differential that can be produced by saidvacuum arrangement is at the highest of the order of one bar. Inaddition to this, the reciprocating piston does, admittedly, exert acertain force, thus causing a corresponding increase in the pressuredifferential effecting the dewatering, but if sufficiently increased,this force will simply push the material out of the extruder, as nocounter-force is provided to prevent this. This means, of course, thatthe total pressure differential across the perforated walls will at themost be of the order of a few bar. This in turn means that the abilityof this previously known method to remove liquid from the spaces betweenthe particles of the material is limited, and in many cases the quantityof the remaining liquid is sufficient: to prevent the shaped bodiesproduced from attaining more structural strength than just needed tokeep their shape against the force of gravity, so that they, unlessextreme care is taken, cannot be handled without deforming, collapsingor falling apart.

[0005] The above problem is, of course, less serious in the case ofshaped bodies of clay, as such bodies can be allowed to or be made toharden respectively by well known methods before being moved, but themethod referred to above is obviously insufficient, if the shaped bodiesare to have a reasonable strength immediately upon having been producedby carrying out the method.

SUMMARY OF THE INVENTION

[0006] It is the object of the present invention to provide a method ofthe kind referred to initially, with which it is possible to produceshaped bodies having a considerable mechanical strength, so that theycan be handled or manipulated mechanically immediately upon completionof the final step of the method without any risk of deforming,collapsing or falling apart.

[0007] By proceeding in this manner, the high pressure differential,produced by applying a high positive pressure to the inside of theperforated walls in the mould, will cause so much of the liquid betweenthe particles to be expelled and the particles to come into such mutualengagement, that a shaped body having a considerable mechanical strengthis produced, and as the slurry has already been homogenized, the shapedbody will have a uniform structure throughout: its volume.

[0008] If the squeezing-out of the liquid occurs at the same time overthe whole surface of the mould, there is a risk that dewatered andun-dewatered material moves about uncontrollably in the moulding spacewith the result that the end product does not become fully homogeneous.This disadvantage may be avoided by proceeding as set forth by the useof a mold, in which the perforations are distributed and adapted in sucha manner so that the liquid will be expressed first from the parts ofthe mold situated most distant from the slurry inlet, then from parts ofthe mold less distant from said inlet, then from parts still closer tothe inlet and so forth, until the complete molding space is occupied byclosely packed and consolidated particulate material forming a compactbody with very low porosity.

[0009] When proceeding in this manner, the final part of the pressingprocess, when no further water can be squeezed out, can be characterizedas powder pressing.

[0010] Thus, the process as such commences in the form of high-pressureslurry pumping in one end of the mould and terminates as apowder-pressing process steadily progressing from the other end of themould. It will be understood that in this case, the low-viscositysuspension will have no difficulty in flowing out into all nooks andcrannies of the mould, and any air having been trapped during thefilling-up of the mould will leave the mould cavity through itsperforations together with the surplus liquid. The finishedpress-moulded object will constitute an accurate replica of the internalsurfaces of the mould, and since the composite material already hassolidified in the mould in the same moment as all surplus water has beensqueezed out and mutual contact between the solid-matter particles hasbeen achieved, it is now possible to remove the moulded object from themould immediately just as with any other powder-pressing method—sincethis object is now fully rigid and self-supporting and requires no morethan being allowed to harden completely by hydration in a suitablemanner.

[0011] Similar results with regard to making the dewatering andconsolidation process progress steadily from one end or side of themould to the other may be achieved by A) using a mold in which theliquid-permeability of the perforations diminishes steadily from the endof the mold most distant from the inlet towards the latter so as to makethe removal of the liquid occur at the highest rate at said distant endand not a steadily diminishing rate when approaching the inlet or B) useof a mold in which the perforations may be closed and opened from theoutside, the removal of the liquid being carried out by opening theperforations in a sequence beginning at the point in the mold mostdistant from the inlet and ending at the latter.

[0012] The perforations or holes in the walls of the moulds should, ofcourse, be extremely fine, so that the water, but not the solid-matterparticles may escape from the mould, but since water molecules areextremely small (approximately 20 Å), this should not be a problem.

[0013] The end product made by proceeding according to one of theembodiments of the method according to the invention is characterized bybeing exceptionally dense and with an absolute minimum of porosity andbeing highly homogeneous, and by, in the fully-hardened condition, topossess valuable physical properties comprising an optimum combinationof strength and toughness.

[0014] Since, as described above, the mixing process is carried out withan arbitrary surplus amount of liquid, and the concentration of thematerial subsequently during the casting or moulding process isincreased without “demixing” taking place, until no more liquid can besqueezed out from the confined material, it is possible in this case toachieve a considerably higher concentration of fibers in the end productthan by using any other known moulding or casting principle, still withthe fibers lying fully dispersed and well distributed and orientedthroughout the product.

[0015] During the terminal part of the pressing process, during whichthe solid particles are closely wedged and pressed together, so that thematerial solidifies, the particles are also pressed firmly against allfiber surfaces—in certain cases even into the surfaces of thefibers—resulting in optimum bond between the fiber and the matrixmaterial and hence optimum fiber effect in the end product.

[0016] In this process, fibers and matrix material “grow together” in amanner not being known from other casting or moulding processes, andafter having fully hardened, the end product possesses unique physicalproperties.

[0017] With uniaxial tension loading, which is the most problematic formof loading to such brittle-matrix materials (because it is difficult forthe fibers to take over the whole: tensional load when the matrix isover-strained), it is possible with a correctly reinforced BMC(Brittle-Matrix-Composite) material produced according to the presentinvention to achieve a stress-strain curve more reminiscent of thestress-strain curve for a metal or for a plastic material than for anordinary brittle matrix material normally exhibiting an ultimateelongation at rupture of only approximately 0.01-0.02 per cent (0.1-0.2mm, per m).

[0018] After hardening, a correctly made BMC material produced accordingto the present invention will have a tensile stress-strain curveexhibiting so-called strain hardening, in which the tensile stresscontinues to increase—without any formation of visible or harmfulcracks—even right up to a strain of 1-2% or more. Thus, thestrainability (elasticity or flexibility if so preferred) of the matrixmaterial has, by extreme utilization of the admixed fibers, beenincreased by a factor of 100 or more—and this without causing any damageto the composite material.

[0019] The mechanism behind the dramatically increased strainability ofthe composite material is that the internal rupturing of the matrixmaterial between the fibers due to tensile straining occurs in adifferent manner than in similar non-reinforced material, as, on amicroscopic level, an evenly distributed pattern of extremely fine andshort microscopic cracks are formed, increasing in number with increasedstraining of the material; these microscopic cracks are, however, sosmall that they may be stopped or blocked by the surrounding fibers, andfor this reason they cause no dramatic damage to the material as such.

[0020] This is in itself extremely valuable and applies in general tothe high-quality BMC materials mentioned above as produced by themethods according to the invention. Further, experience has shown thatfor so-called FRC material produced with a normal Portland-cementmatrix, the network of micro-cracks formed in the manner referred toabove (with possible crack lengths of approximately 0.5-1 mm or less,width typically 10-50 gm) after being formed shows a marked tendency toself-healing, so that the material in the presence of moisture willagain be dense, and so that the material when again being tension loadedachieves its original rigidity and strength and may be subjected toincreased stresses in the same manner as during the first loading, alsohere exhibiting a smooth stress-strain curve and a convincing strainhardening with steadily increasing tensile stresses up to an ultimatestraining capacity of 1-2% or more before the stresses begin todecrease.

[0021] The present invention also relates to an apparatus for carryingout the method of the invention.

[0022] Finally, the invention relates to a product, comprising anon-flowable body of consolidated closely-packed particles of solidmaterials produced by the method and/or apparatus of the invention.

[0023] Advantageous embodiments of the method and the apparatus, theeffects of which—beyond what is self-evident—are explained in thefollowing detailed part of the present description.

BRIEF DESCRIPTION OF THE DRAWINGS

[0024] In the following detailed portion of the present description, theinvention will be explained in more detail with reference to thedrawings.

[0025]FIG. 1 is a diagrammatic. longitudinal sectional view through theparts of an extruder relevant to the invention.

[0026]FIG. 2 shows an example of the formation of draining openings inthe part of the extruder wall constituting the drainage section.

[0027]FIG. 3 is a sectional view through a ring adapted to co-operatewith a number of similar rings to form an extruder wall with drainingslits.

[0028]FIG. 4 shows a part of an extruder wall composed of a number ofrings of the kind shown in FIG. 3.

DESCRIPTION OF THE PREFERRED EMBODIMENT

[0029]FIG. 1 shows the parts of an extruder essential to the invention,specially, designed for producing tubular products, it being obviousthat an extruder based on the same principles could also be used forextruding products with other cross-sectional shapes, such as flat orcorrugated sheets or profiled stock of various cross-sectional shapes.

[0030] The parts of the extruder shown comprise an outer part 1, aninner part 2, a plurality of nozzles or slits 3 for draining-off liquid,as well as a pressure-regulating chamber 5.

[0031] As shown, the extruder is divided into four consecutive sections,i.e.

[0032] an inlet section A for the supply of flowable suspension to becompacted, and

[0033] a flow section B, in which the suspension having been suppliedflows towards

[0034] a drainage and consolidation section C leading into

[0035] a solid-friction section D.

[0036] Further, FIG. 1: shows a further section, designated the exitsection E, in which the extruded product leaves the extruder.

[0037] For ease of understanding, FIG. 1 shows the above-mentionedsections as quite distinct from each other, but in practice, two or moresections may overlap to a greater or lesser degree. Thus, the nozzles 3,shown in FIG. 1 as solely being present in the drainage andconsolidation section C, may well also extend along at least a part ofthe solid-friction section D.

[0038] In the inlet section A, a flowable suspension containing therequisite amounts of powder, liquid (normally water) and possiblyfurther components flows into the flow section B. The suspensionsupplied to the extruder comprises a surplus of water or other liquid,making it possible to achieve a good and homogeneous intermixing of thecomponents of the suspension, that may have a consistency ranging from athin slurry to a thick paste. Preferably, the ratio between liquid anddry matter is 1:1.

[0039] The mixing process may be carried out in a manner known per se,i.e. by using a high-performance mixer producing a paste-like particlesuspension with the desired flowability, prior to supplying the latterto the inlet section A of the extruder by means of a high-pressure pumpof a type capable of pumping material of this kind.

[0040] From the inlet section A, the suspension flows in the forwarddirection through the flow section B. The cross-sectional shape of theshaped product in this section B and the subsequent drainage andconsolidation section C is determined by the internal shape of the outerpart 1 and the external shape of the inner part 2. In the drainage andconsolidation section C, surplus liquid is drained off, and thesuspension is consolidated to form a solid material with direct contactbetween the individual particles throughout the product, assubstantially all surplus liquid, i.e. substantially all liquid notremaining to occupy the interspaces between the closely packed particlesin direct mutual contact, is removed. This draining-off function iscaused by the pressure differential across the outer part 1 in thedrainage and consolidation section C being applied to the nozzles orslits 3. The pressure differential constitutes the difference between onthe one hand the hydrostatic pressure in the suspension in the flowsection B and part of the drainage and consolidation section C, whichmay lie in the range of 20-400 bar, and on the other hand the pressurewithin the pressure-regulating chamber 5, that may be atmosphericpressure or somewhat higher or lower, as will be explained below.

[0041] Obviously, the high hydrostatic pressure reigning in the flowsection B and at least the adjacent part of the drainage andconsolidation section C can only be maintained, if the part of theextruder downstream of the drainage and consolidation section Ccomprises some means of obstructing flow. In the method according to thepresent invention, these means are provided by the non-flowable extrudedproduct resulting from the drainage and consolidation described above,being present in the solid-friction section D. In this section D, thefriction between the product 4 and the walls of the outer part 1 and theinner part 2 in contact with it is sufficient to provide a reactionforce of substantially the same magnitude as the oppositely actinghydraulic force resulting from the hydraulic pressure upstream of thesolid-friction section D. In operation, the supply pressure and thepressure in the pressure-regulating chamber 5 are attuned to each otherand to the friction referred to in the solid-friction section D so as toallow the product 4 to advance at a suitable speed.

[0042] When the product 4 leaves the extruder in the exit section E, itsporosity is extremely low and it contains substantially no more liquidthan that occupying the interspaces between the closely packedparticles, so that the product 4 is now rigid and has a sufficientdimensional stability to withstand handling during the subsequentprocessing without being deformed due to its own weight. Such subsequentprocessing may i.e. be firing in the case of a product containing clay,or hardening in the case of a product based on cement.

[0043] When starting-up the process, it is necessary to provide thereaction force referred to above by separate means, as the non-flowableproduct part has not yet been formed in the solid-friction section D.This may suitably be achieved by inserting a reaction-force plug (notshown) into the downstream end of the interspace between the outer part1 and the inner part 2 so as to effect a temporary closure.

[0044] As soon as the non-flowable “plug” of consolidated material hasbeen formed in the solid-friction section D, it will normally provide asufficient reaction force, but will on the other hand, of course,require a considerable force to act upon it to overcome the frictionagainst the extruder walls and move it forward.

[0045] With an extruder constructed according to the principle shown inFIG. 1, it may not always be possible to attune the pressures referredto above in such a manner, that the consolidated product in thesolid-friction section D will be moved, as an increase in the supplypressure, i.e. an increase in the inlet section A and in the flowsection B, may, cause the friction between the consolidated product andthe extruder walls to produce a reaction force that will always be toohigh. The effects of this high frictional force may be reduced in anumber of different ways to be explained below.

[0046] A first method of reducing the effect of friction between theconsolidated material and the walls of the extruder consists insubjecting the exit portion of the extruder or a part of same tomechanical vibrations. The frequency of these vibrations may lie in theinterval 10-400 Hz, while the interval 20-200 Hz is preferred and theinterval 50-150 Hz is more preferred.

[0047] Another method of reducing the effect of the high frictionreferred to above is to subject the flowable suspension upstream of theconsolidated product to pressure variations, so that periods with afirst, lower pressure alternate with second, shorter periods with asecond, higher pressure, said second pressure being approximately 1.58,preferably 2-4 times greater than said first pressure.

[0048] A third method of reducing the effect of the high frictionreferred to above is to vary the pressure in the pressure regulatingchamber 5, so that the surface of the product in some periods issubjected to reduced pressure to support the draining-off process, andin other periods being subjected to a high-pressure to reduce thefriction between the product and the extruder walls.

[0049] A fourth method of reducing the effect of the high frictionreferred to above is based on using an extruder, in which a first part,i.e. the outer part 1 shown in FIG. 1, is capable of being reciprocatedin the longitudinal direction relative to another part of the extruder,e.g. the inner parts 2. With such relative movement, that may e.g. beeffected by using a crank mechanism (not shown), the product 4 will bemade to “walk” stepwise in the downstream direction. The stepwise“walking” movement of the product is achieved through the followingmechanism: when both parts of the extruder are stationary, the resultingfrictional force between the product and the extruder walls will act inthe upstream direction with a magnitude always equal to the resultingforce on the product in the downstream direction from the pressure inthe flowable suspension.

[0050] However, when the movable part of the extruder is moved in thedownstream direction, the friction stresses between the product and themovable extruder wall will change direction and result in a frictionalforce in the downstream direction. In this situation it is possible toattune the pressure in the flowable suspension in such a way that theresulting frictional force acting in the downstream direction togetherwith the resulting force from the pressure in the flowable suspension islarger than or equal to the resulting frictional force acting in theupstream direction, thus causing the product to move in the downstreamdirection.

[0051] When the movement of the extruder is stopped or changed to theupstream direction, the resulting frictional forces on the product fromboth parts of the extruder will again act in the upstream directioncausing the movement of the product to stop. It follows from the abovethat an extruder working according to this principle should be designedtaking into consideration the cross-sectional area of the product, theworking pressure in the flowable suspension and the size and frictionalcharacteristics of on the one hand the surface between the stationarypart of the extruder and the product and on the other hand the surfacebetween the movable part of the extruder and the product.

[0052]FIG. 2 shows one example of how the requisite permeability of theextruder wall in the drainage and consolidation section C may beachieved. Thus, in the outer part 1 a number of holes 6 have beendrilled into the outer part 1 from the outside. As shown, the holes 6only extend to within approx. 1 mm from the inside wall 7. In thelatter, a plurality of extremely fine perforations 8 with transversedimensions of the order of 0.001-0.01 mm extend through the respectivedrilled holes 6. The perforations 8 may be produced by means of e.g.spark erosion or by using a laser beam. FIG. 2 also shows the centralaxis 9 of the extruder.

[0053] Another way of providing the requisite openings in the drainageand consolidation section C is shown in FIGS. 3 and 4. Thus, FIG. 3shows a ring to be used for this purpose, and FIG. 4 shows how a numberof such rings are assembled to form a number of slits constituting saidopenings.

[0054] The ring 12 shown in FIG. 3 comprises an inner periphery 10 andan outer periphery 11. The width b₁ of the inner periphery 10 is atrifle, typically approximately 0.0010.01 mm, less than the width b2 ofthe outer periphery 11. Thus, when a number of rings 12 are clampedaxially together in the extruder, slits 3 will be formed between themwith a width of typically approximately 0.001-0.01 mm in the drainageand consolidation section C, through which the liquid to be drained offmay escape. FIG. 4 shows a number of rings 12 of the kind shown in FIG.3 mounted in the axial direction in the outer part 1 of the extruder, sothat the inner peripheries 10 of the rings are aligned with the insidesurface of the outer part 1 of the extruder. FIG. 4 shows the outerparts 1 and a plurality, in this case a total of six, individual rings12 with the drainage slits 3 between the rings. The central axis 9 ofthe extruder will also be seen.

We claim:
 1. A method for producing shaped bodies in which all surfacesare formed by an extruder comprising the steps of: (a) forming aflowable suspension of particulate material in a suitable liquid as aneasily flowable moulding slurry wherein said liquid occupies interspacesbetween said particulate material; (b) introducing said suspension intoa complete moulding space with at least partly liquid-permeable walls;(c) removing at least a major proportion of said liquid by establishinga pressure differential across at least parts of said walls that arepermeable to said liquid, so as to form in said complete moulding spacea non-flowable, shaped body of said material; and (d) removing saidnon-flowable, shaped body from said complete moulding space; and whereinsteps (b) and (c) above are carried out by pumping said slurry into aclosed extruder defining said complete moulding space and having aslurry inlet such that the method commences as a high-pressure slurrypumping process and terminates as a powder-pressing process and byapplying a sufficiently high pressure to said slurry in said extruder toestablish said pressure differential with a magnitude of 50-400 bar toconsolidate said particulate material into said non-flowable, shapedbody, whereby substantially all of said liquid in said interspaces isexpelled from said complete moulding space such that said particulatematerial in said complete moulding comes into close mutual engagementand said complete moulding space is occupied by closely packed andconsolidated particulate material forming said non-flowable, shaped bodyhaving very low porosity, a uniform structure and considerablemechanical strength to thereby provide form stable bodies havingsufficient mechanical strength to be handled immediately after leavingsaid extruder.
 2. The method according to claim 1, wherein perforationsare distributed in the at least partly liquid permeable walls so thatsaid liquid is expressed first from the complete moulding space situatedmost distant from the slurry inlet, then from the complete mouldingspace less distant from said inlet, then from the complete mouldingspace still closer to said inlet, until the complete moulding space inits entirety is occupied by closely packed and consolidated particulatematerial forming a compact body with very low porosity.
 3. The methodaccording to claim 2, wherein liquid-permeability of said perforationsdiminishes steadily from an end of the complete moulding space mostdistant from the inlet towards the inlet so as to make the removal ofthe liquid occur at a highest rate at said most distant end and at asteadily diminishing rate when approaching the inlet.
 4. The methodaccording to claim 1, wherein said flowable suspension containsparticulate material selected from the group consisting of materialscontaining clay, materials based on hydraulic cement, calcium-silicatematerials and materials containing gypsum.
 5. The method according toclaim 1, wherein perforations in the walls are closed and opened fromoutside, the removal of the liquid being carried out by opening theperforations in a sequence beginning at a point in the complete mouldingspace most distant from the inlet and ending at the inlet.
 6. The methodaccording to claim 1, further comprising passing said suspension throughan extrusion duct of the extruder, the extrusion duct defining thecomplete moulding space and having a substantially constantcross-sectional shape and size, and removing liquid from the suspensionby means of a pressure differential across parts of walls of theextrusion duct having openings allowing said liquid but not theparticles to leave the extrusion duct so as to convert the suspension tothe non-flowable body having a cross-sectional shape corresponding tothe cross-sectional shape of the extrusion duct, wherein the pressuredifferential is established and maintained by applying a highsuper-atmospheric pressure to said suspension at or upstream of itsentry into the extrusion duct and applying or permitting a substantiallylower pressure to reign on an exit side of said openings, and whereinthe pressure differential and the liquid-out-flow capability of saidopenings are mutually attuned so that a part of said non-flowable bodyat any time downstream-most in the extrusion duct engages the walls ofthe extrusion duct with a frictional force sufficient to withstand saidpressure applied to the suspension.
 7. The method according to claim 6,wherein the pressure differential and the liquid-oufflow capability ofsaid openings are mutually attuned so that said frictional force allowssaid non-flowable body to move in a downstream direction under aninfluence of said pressure applied to the suspension.
 8. The methodaccording to claim 6, wherein the downstream part of the extrusion ductis subjected to vibration in order to reduce an effect of frictionbetween the consolidated material and the extrusion duct walls.
 9. Themethod according to claim 6, wherein the flowable suspension upstream ofdrained and consolidated material is subjected to varying pressure, sothat periods with a first, lower pressure alternate with shorter periodswith a second higher pressure, said second higher pressure beingapproximately 1.5-8 times greater than said first pressure.
 10. Themethod according to claim 6, wherein a surface of the non-flowable bodyis subjected to varying pressure from a pressure-regulating chambersurrounding a draining section.
 11. The method according to claim 6,wherein a shaping part of said extrusion duct is divided longitudinallyinto at least two parts, that are reciprocated relative to each other ina longitudinal direction in order to ease forward movement of theconsolidated material.
 12. The method according to claim 11, wherein theshaping part of the extrusion duct is divided longitudinally into twoparts, one of said parts being fixed and the other of said parts beingreciprocated in the longitudinal direction.
 13. The method according toclaim 1, wherein the liquid is drained off through pores or slits with adiameter or width of less than approximately 0.5 mm.
 14. The methodaccording to claim 1, wherein the flowable suspension contains fibersdistributed in the suspension as well as in the consolidated material ofthe non-flowable body.
 15. The method according to claim 6, wherein thefibers are oriented in a desired manner throughout at least a part of across-section of the consolidated material of the non-flowable body byadjusting conditions of introduction and consolidation of thesuspension, and wherein an introduction of the suspension through theslurry inlet having a converging cross-sectional shape results in atendency to an axial orientation of the fibers, and an introduction ofthe suspension through the slurry inlet which is tangentially directedresults in a tendency to a tangential orientation of the fibers.
 16. Themethod according to claim 15, wherein the fibers are high-strengthfibers, selected from the group consisting of carbon fibers, cellulosefibers, steel fibers, glass fibers, polyolefin fibers, polypropylenefibers and ultra-fine fibers and wherein the degree of reinforcementexpressed as the fiber volume fraction in said consolidated, shaped bodyis 1-15%.
 17. The method according to claim 1 wherein the step ofremoving said non-flowable, shaped body from said complete mouldingspace by reducing effects of friction comprises subjecting at least apart of an exit portion of the extruder to mechanical vibrations. 18.The method according to claim 1 wherein the step of removing saidnon-flowable, shaped body from said complete moulding space by reducingeffects of friction comprises subjecting the flowable suspension topressure variations.
 19. The method according to claim 1 wherein thestep of removing said non-flowable, shaped body from said completemoulding space by reducing effects of friction comprises varying thepressure differential applied to a surface of the material during saidstep of removing at least a portion of said liquid.
 20. The methodaccording to claim 1 wherein the step of removing said non-flowable,shaped body from said complete moulding space by reducing effects offriction comprises reciprocating portions of the extruder in alongitudinal direction.
 21. The method according to claim 1, wherein theflowable suspension comprises cementitious material, liquid andreinforcing fibers.
 22. A method of producing a fiber reinforcedcementitious body, said method including the steps of: (a) forming aflowable slurry comprising cementitious material, liquid and reinforcingfibers; (b) introducing said flowable slurry into an extruder includingwalls defining a moulding space, at least part of said walls beingpermeable to said liquid; (c) applying a sufficiently high pressure tosaid slurry in said extruder to establish a pressure differential with amagnitude of 50-400 bar across at least said liquid permeable part ofsaid walls to consolidate said cementitious material and fibers into anon-flowable shaped body where a major portion of said liquid isexpelled from said moulding space and the cementitious material isforced into engagement with said fibers; and (d) removing saidnon-flowable body from said molding space.
 23. The method according toclaim 22: wherein said cementitious material includes particles; andwherein said applying step includes, during a terminal part thereof, thepressing of the particles firmly against all surfaces of the fibers toproduce an optimum bond between the fibers and the particles and hencean optimum fiber effect in the non-flowable body.
 24. The methodaccording to claim 23, wherein said pressing includes the pressing ofthe particles into the fibers.
 25. The method according to claim 22,wherein perforations are distributed in the permeable at least part ofsaid walls so that said liquid is expressed first from the mouldingspace situated most distant from a slurry inlet, then from the mouldingspace less distant from said inlet, then from the moulding space stillcloser to said inlet, until the moulding space in its entirety isoccupied by closely packed and consolidated cementitious materialforming a compact cementitious body with very low porosity.
 26. Themethod according to claim 25, wherein liquid-permeability of saidperforations diminishes steadily from an end of the moulding space mostdistant from the inlet towards the inlet so as to make the removal ofthe liquid occur at a highest rate at said most distant end and at asteadily diminishing rate when approaching the inlet.
 27. The methodaccording to claim 22, wherein said flowable slurry contains particulatematerial selected from the group consisting of materials containingclay, materials based on hydraulic cement, calcium-silicate materialsand materials containing gypsum.
 28. The method according to claim 22,wherein perforations in the permeably at least part of said walls areclosed and opened from outside, the removal of the liquid being carriedout by opening the perforations in a sequence beginning at a point inthe moulding space most distant from an inlet and ending at the inlet.29. The method according to claim 22, further comprising passing saidflowable slurry through an extrusion duct of the extruder, the extrusionduct having a substantially constant cross-sectional shape and size, andremoving liquid from the flowable slurry by a pressure differentialacross the permeable at least part of said walls of the extrusion ducthaving openings allowing said liquid but not the cementitious materialand fibers to leave the extrusion duct so as to convert the slurry tothe non-flowable body having a cross-sectional shape corresponding tothe cross-sectional shape of the extrusion duct, wherein the pressuredifferential is established and maintained by applying a highsuper-atmospheric pressure to said slurry at or upstream of its entryinto the extrusion duct and applying or permitting a substantially lowerpressure to reign on an exit side of said openings, and wherein thepressure differential and a liquid-out-flow capability of said openingsare mutually attuned so that a part of said non-flowable body at anytime downstream-most in the extrusion duct engages the walls of theextrusion duct with a frictional force sufficient to withstand saidpressure applied to the suspension.
 30. The method according to claim29, wherein the pressure differential and the liquid-outflow capabilityof said openings are mutually attuned so that said frictional forceallows said non-flowable body to move in a downstream direction under aninfluence of said pressure applied to the suspension.
 31. The methodaccording to claim 29, wherein a downstream part of the extrusion ductis subjected to vibration in order to reduce an effect of frictionbetween the non-flowable body and the extrusion duct walls.
 32. Themethod according to claim 29, wherein the flowable slurry upstream ofthe non-flowable body is subjected to varying pressure, so that periodswith a first, lower pressure alternate with shorter periods with asecond higher pressure, said second higher pressure being approximately1.5-8 times greater than said first pressure.
 33. The method accordingto claim 29, wherein a surface of the non-flowable body is subjected tovarying pressure from a pressure-regulating chamber surrounding adraining section.
 34. The method according to claim 29, wherein ashaping part of said extrusion duct is divided longitudinally into atleast two parts, and said at least two parts are reciprocated relativeto each other in a longitudinal direction in order to ease forwardmovement of the consolidated material.
 35. The method according to claim34, wherein the shaping part of the extrusion duct is dividedlongitudinally into two parts, one of said parts being fixed and theother of said parts being reciprocated in the longitudinal direction.36. The method according to claim 29, wherein the fibers are oriented ina desired manner throughout at least a part of a cross-section of thenon-flowable body by adjusting conditions of introduction andconsolidation of the slurry, and wherein an introduction of the slurrythrough a slurry inlet having a converging cross-sectional shape resultsin a tendency to an axial orientation of the fibers, and an introductionof the slurry through the slurry inlet which is tangentially directedresults in a tendency to a tangential orientation of the fibers.
 37. Themethod according to claim 22, wherein the liquid is drained off throughpores or slits with a diameter or width of less than approximately 0.5mm.
 38. The method according to claim 22, wherein the fibers areoriented in a desired manner throughout at least a part of across-section of the non-flowable body by adjusting conditions ofintroduction and consolidation of the slurry, and wherein anintroduction of the slurry through a slurry inlet having a convergingcross-sectional shape results in a tendency to an axial orientation ofthe fibers, and an introduction of the slurry through the slurry inletwhich is tangentially directed results in a tendency to a tangentialorientation of the fibers.
 39. The method according to claim 22, whereinthe fibers are high-strength fibers, selected from the group consistingof carbon fibers, cellulose fibers, steel fibers, glass fibers,polyolefin fibers, polypropylene fibers and ultra-fine fibers, andwherein the degree of reinforcement expressed as the fiber volumefraction in said consolidated, shaped body is 1-15%.
 40. The methodaccording to claim 22 wherein the step of removing said non-flowablebody from said moulding space includes reducing effects of friction bysubjecting at least a part of an exit portion of the extruder tomechanical vibrations.
 41. The method according to claim 22 wherein thestep of removing said non-flowable body from said moulding spaceincludes reducing effects of friction by subjecting the flowablesuspension to pressure variations.
 42. The method according to claim 22wherein the step of removing said non-flowable body from said mouldingspace includes reducing effects of friction by varying the pressuredifferential applied to a surface of the non-flowable body during saidstep of applying step which removes at least a portion of said liquid.43. The method according to claim 22 wherein the step of removing saidnon-flowable body from said moulding space includes reducing effects offriction by reciprocating portions of the extruder in a longitudinaldirection.